Page 268 - Formation Damage during Improved Oil Recovery Fundamentals and Applications
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Formation Damage by Inorganic Deposition                     239


              adsorption or precipitation on the rock surface or other mechanisms.
              After the well is placed back on production, the inhibitor slowly dissolves
              or desorbs from the rock and enters the produced water and sea water
              over time.
                 As the squeezed chemicals flow back into the well with the produced
              fluids, the inhibitors inhibit the formation of scale from the sand face to
              the topside facilities. Ideally, the inhibitor will return over a period of
              weeks or months at a low concentration just above the minimum inhibi-
              tor concentration (MIC) that is required to prevent scaling (Graham
              et al., 2005). The MIC is linked to the severity of the scale problem
              depending on the ratio of sea water and produced water and the concen-
              tration of scaling ions in the formation water. A high MIC could lead to
              more frequent treatments. However, the limitations of the methods have
              become apparent in more challenging environments such as deepwater or
              remote wells because these wells usually require intervention-free and
              totally reliable scale-prevention strategies are demanded. Scale inhibitor
              treatment frequencies are typically 2 3 per year per well depending on
              the volume of produced water treated. Squeeze lifetimes are sometimes
              referred to in total barrels of produced water treated. The squeeze life-
              time is strongly influenced by the severity of the scaling environment,
              inhibitor chemistry, the MIC, and the formation properties. The general
              industry experience is that the first squeeze treatments performed on a
              well give the shortest lives leading to a higher intervention frequency
              during early sea water breakthrough.
                 Fig. 5.13 shows a typical scale inhibitor squeeze treatment. In the pre-
              flush stage, typically of about 50 barrels of flush fluid mixture is injected.
              The preflush fluids usually contain some biocide and scale inhibitors up
              to 200 ppm. The purpose of a preflush is to maximize the fluid contact
              with rock to reduce near wellbore damage. After the preflush, the main
              inhibitor treatment will be started with a volume of 250 to 500 barrels
              based on the treatment design. Following the main treatment, about 500
              barrels or more fluid will be injected to ensure the accurate placement of
              chemicals. A typical treatment is usually less than 30 ft from the wellbore,
              and the reservoir gross thickness significantly affects the actual volume
              needed for each stage of injection during the squeeze treatment.
                 Some potential drawbacks of the squeeze technology should be taken
              into consideration before it is used. Firstly, squeeze lifetime is finite for a
              particular volume of water production, which indicates that wells need to
              be treated periodically to maintain scale control. Secondly, squeeze
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